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EP0382009B1 - Membrane semiperméable d'un alliage polymère mélangé demanière - Google Patents

Membrane semiperméable d'un alliage polymère mélangé demanière Download PDF

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Publication number
EP0382009B1
EP0382009B1 EP90101455A EP90101455A EP0382009B1 EP 0382009 B1 EP0382009 B1 EP 0382009B1 EP 90101455 A EP90101455 A EP 90101455A EP 90101455 A EP90101455 A EP 90101455A EP 0382009 B1 EP0382009 B1 EP 0382009B1
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EP
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Prior art keywords
membrane
group
phenylene
alkyl
polymer blend
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Expired - Lifetime
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EP90101455A
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German (de)
English (en)
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EP0382009A1 (fr
Inventor
Michael Dr. Haubs
Willi Dr. Kreuder
Claus-Peter Dr. Krieg
Jürgen Wildhardt
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Hoechst AG
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Hoechst AG
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
    • B01D67/0081—After-treatment of organic or inorganic membranes
    • B01D67/0083—Thermal after-treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
    • B01D71/06—Organic material
    • B01D71/56—Polyamides, e.g. polyester-amides

Definitions

  • the invention relates to a semipermeable membrane made of a homogeneously mixed polymer alloy, which contains polyamide and polyvinylpyrrolidone as main constituents, and to a process for their production.
  • EP-A-0 082 433 provides a clear presentation of the advantages and disadvantages of membranes which are already known. For example, there are hydrophilic, asymmetrical cellulose acetate membranes with satisfactory anti-adsorptive properties, which leave much to be desired in terms of their thermal and chemical resistance. Membranes made of polysulfones or similar polymers have good thermal and chemical resistance, but because of the hydrophobic properties of the polymers used, such membranes have a pronounced tendency to adsorb solutes, which virtually clogs the membrane.
  • EP-A-0 082 433 describes membranes made of a hydrophilic and a hydrophobic component.
  • Polysulfones, polyether sulfones, aromatic and araliphatic polyamides are described as hydrophobic components.
  • PVP with a molecular weight (MW) of at least 100,000 daltons is mentioned as the hydrophilic component.
  • MW molecular weight
  • the high MW ensures that the PVP is built into the membrane during the precipitation process and is not removed again.
  • organic solvents There are also problems with these membranes when they are used in wastewater treatment; if so-called silicone defoamers are present in the wastewater, then these membranes clog.
  • US-A-4 051 300 describes membranes which are composed of polysulfone or of polyamide.
  • PVP is added to the casting solution as a viscosity-regulating component and washed out again after the precipitation.
  • hydrophobic membranes with good thermal properties and good chemical resistance are available, which, however, have a pronounced tendency to absorb solutes due to their lack of hydrophilicity.
  • Hydrophilicity and resistance to solvents are found in membranes made from regenerated cellulose; however, these are relatively easy to hydrolyze in acidic or alkaline media and, moreover, they are easily attacked by microorganisms.
  • the invention has for its object to provide semipermeable membranes which have pronounced hydrophilic properties, i. H. are able to absorb significant amounts of water, based on their total weight, which are resistant to saponifying and oxidative agents as well as to thermal influences, which resist organic solvents better than membranes made of hydrophobic polymer, which show low protein adsorption, which have good wettability and which are also insensitive to the action of microorganisms.
  • the aromatic polyamide expediently used for the membrane according to the invention can be present both as a random copolymer and as a block or graft copolymer.
  • the following compounds are particularly suitable for producing the aromatic polyamides having the recurring structural units of the formula (I): as dicarboxylic acid derivatives of the formula Cl - CO - Ar1 - CO - Cl 4,4'-Diphenylsulfondicarbonklaredichlorid, 4,4'-Diphenyletherdicarbonklaredichlorid, 4,4'-Diphenyldicarbonklaredichlorid, 2,6-Naphthalindicarbonklaichlorid, Isophthal Acidichlorid, but especially terephthalic acid dichloride and substituted terephthalate.
  • dicarboxylic acid derivatives of the formula Cl - CO - Ar1 - CO - Cl 4,4'-Diphenylsulfondicarbonklaichlorid, 4,4'-Diphenyletherdicarbonklaichlorid, 4,4'-Diphenyldicarbonklaichlorid, 2,6-Naphthalindicarbonklaichlorid,
  • 2-chloro-terephthalic acid dichloride as aromatic diamines of the structure H2N-Ar1-NH2 m-phenylenediamines or substituted phenylenediamines, e.g. B. 2-chloro, 2,5-di-chloro or 2-methoxy-p-phenylenediamine, especially p-phenylenediamine; as substituted benzidine derivatives 3,3'-dimethoxy, 3,3'-di-chloro, 2,2'-dimethyl and preferably 3,3'-dimethylbenzidine; as diamine components of the formula H2N-Ar1-X-Ar2-NH2 4,4'-diaminobenzophenone, bis [4-aminophenyl] sulfone, bis [4- (4'-aminophenoxy) phenyl] sulfone, 1,2-bis [4'-aminophenoxy] benzene, 1,4-bis [(4'-amin
  • Polyaramides can be prepared in a known manner by solution, interface or melt condensation.
  • the solution condensation of the aromatic dicarboxylic acid dichlorides with the aromatic diamines takes place in aprotic, polar solvents of the amide type such as, for. B. in N, N-dimethylacetamide or in particular in N-methyl-2-pyrrolidone. If appropriate, these solvents can be added in a known manner to increase the solvency or to stabilize the polyamide solutions, halide salts of the first and / or second group of the periodic system.
  • Preferred additives are calcium chloride and / or lithium chloride.
  • the polycondensation temperatures are usually between -20 ° C and +120 ° C, preferably between +10 ° C and +100 ° C. Particularly good results are achieved at reaction temperatures between +10 ° C and +80 ° C.
  • the polycondensation reactions are preferably carried out such that 2 to 30, preferably 6 to 15% by weight of polycondensate are present in the solution after the reaction has ended.
  • the polycondensation can in the usual manner, for. B. by adding monofunctional compounds such. B. Benzoyl chloride can be stopped.
  • the hydrogen chloride formed and loosely bound to the amide solvent is neutralized by adding basic substances. Suitable for this are, for example, lithium hydroxide, calcium hydroxide, but in particular calcium oxide.
  • the Staudinger index is a measure of the average chain length of the resulting polymers.
  • the Staudinger index of membrane-forming aromatic polyamides should be between 50 and 1,000 cm3 / g, preferably between 100 and 500 cm3 / g, particularly preferably between 150 and 350 cm3 / g. It was determined on solutions of 0.5 g of polymer in 100 ml of 96% sulfuric acid at 25 ° C.
  • the alloys can be removed by removing the solvent, e.g. B. by evaporation, isolated and processed into intermediates (granules or powder), which can then be used as raw materials for membrane production.
  • solvent e.g. B. by evaporation
  • the molecular weight of the PVP is generally from 1,000 to 3 million, preferably from 40,000 to 200,000, in particular from 50,000 to 100,000.
  • the alloys of the invention are polymer mixtures, the components of which are homogeneously mixed in all proportions.
  • the alloys contain PVP in amounts of 1 to 80% by weight, preferably 5 to 60% by weight and particularly preferably 10 to 50% by weight, based on the sum of the components (a + b).
  • polymer alloys described above are not, as such, the subject of the present invention, but are described in detail in a patent application filed with the same priority in connection with moldings. Rather, the invention relates to a semipermeable membrane containing said polymer alloy as the main component.
  • the solution of the alloy already described is filtered, degassed, and then in a known manner by the phase inversion method (Robert E. Kesting, "Synthetic Polymeric Membranes", 2nd Ed., 1985, p. 237 ff .) made a semipermeable membrane.
  • the polymer solution is spread out on a flat surface as possible as a liquid layer.
  • the flat base can consist, for example, of a glass plate or a metal drum.
  • precipitation liquid is allowed to act on the liquid layer, which is miscible with the solvent of the solution, but in which the polymers dissolved in the polymer solution are precipitated as a membrane.
  • Water for example, is used as the precipitation liquid.
  • the precipitating liquid is advantageously allowed to act on the membrane precipitated by it until practically all of the solvent is replaced by precipitating liquid. Then the membrane formed is freed of precipitation liquid, for example by drying the membrane directly in an air stream or first treating it with a plasticizer such as glycerol and then drying it.
  • membranes which are arranged on a carrier layer which is permeable to flowable media
  • a nonwoven e.g. B. made of plastic, or a paper and leaves this after formation of the membrane layer on the base.
  • the membrane can also initially be produced without a carrier and only then applied to a permeable carrier.
  • Hollow threads or capillaries can also be produced in a known manner from the solution of the polymer alloy by spinning the polymer solution according to the prior art into a precipitation liquid through a suitably designed shaping annular gap or hollow needle nozzle.
  • the production conditions can be selected so that an outer or inner skin or both are formed.
  • the wall thickness of such capillaries or hollow fibers is usually in the range from 20 to 500 »m.
  • the membrane is impregnated with glycerol after the coagulation, it can preferably contain in the range from 5 to 60% glycerol, based on its total weight; the membrane thus impregnated is dried, e.g. B. at a temperature of 50 ° C.
  • the membrane according to the invention is also suitable as a carrier membrane for permselective layers which are produced directly on or in the membrane.
  • permselective layers which are produced directly on or in the membrane.
  • “Ultra-thin” layers ( ⁇ 1 »m) of polymers with functional groups e.g. silicones, cellulose ethers, fluoropolymers
  • the membrane according to the invention is also suitable as a carrier of reactive molecules, for example in order to fix enzymes or anticoagulants such as heparin according to the prior art.
  • the thickness of the membrane according to the invention without a support layer is in the range from 10 to 300 »m, in particular from 20 to 120» m.
  • a heat treatment of the membrane can surprisingly result in a subsequent change in the membrane properties.
  • Examples 2 and 4 show how a very substantial increase in the retention capacity for dissolved substances is made possible by placing the membrane in hot water (100 ° C.).
  • a 2% aqueous solution of polyvinylpyrrolidone (PVP) was used as the test solution, available under the name "Kollidon K30" (R) from BASF, the molar mass of the polyvinylpyrrolidone was 49,000 daltons.
  • the concentration measurements were carried out in a digital density meter "DMA 60 + 601" (R) from Heraeus.
  • the membranes of Examples 1 to 3 were placed in acetone for one hour in order to exchange the liquid contained in the pores of the membranes for acetone.
  • the membranes were then exposed to the solvents listed in Table 2 at a temperature of 25 ° C. for a period of 12 h.
  • the membranes were then reconditioned to water and, as stated in Example 1, the mechanical permeability and the retention capacity were measured on the membranes treated with the organic solvents.
  • the results are shown in Table 2 and show that the deviations from the values given in Table 1 are within the tolerance limits of the measuring method.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Claims (23)

  1. Membrane semi-perméable à base d'un alliage de polymères mélangés de façon homogène, contenant en tant que composants principaux un polyamide aromatique et une polyvinylpyrrolidone, le polyamide aromatique étant un homo- ou copolyaramide comportant au moins un motif structural répété de formule (I)
    Figure imgb0025
     dans laquelle E¹ et E² sont identiques ou différents et sont choisis parmi les groupements
    Figure imgb0026
     -Ar¹-
    -Ar¹-X-Ar²-,
    dans lesquels Ar¹ et Ar² sont des radicaux 1,2-phénylène, 1,3-phénylène ou 1,4-phénylène identiques ou différents, qui peuvent être substitués par des groupes alkyle en C₁-C₆, alcoxy en C₁-C₆, -CF₃ ou par des atomes d'halogène, et le radical X
    a) est une liaison directe ou représente l'un des radicaux bivalents suivants
    -O-, -C(CF₃)₂-, -SO₂-, -CO-, -C(R¹)₂-, dans lequel R¹ est un atome d'hydrogène ou un groupe alkyle en C₁-C₆ ou fluoroalkyle ayant de 1 à 4 atomes de carbone dans le fragment alkyle, ou
    b) représente un groupe -Z-Ar¹-Z- dans lequel Z est le radical -O- ou -C(CH₃)₂, ou
    c) représente un groupe -O-Ar¹-Y-Ar²-O- dans lequel Y a la signification donnée en a).
  2. Membrane selon la revendication 1, caractérisée en ce que l'halogène est le fluor, le chlore ou le brome.
  3. Membrane selon la revendication 1 ou 2, caractérisée en ce que le groupement E¹ est le même ou est différent dans les motifs structuraux et représente un radical 1,3- ou 1,4-phénylène ou le radical
    Figure imgb0027
  4. Membrane selon la revendication 1 ou 2, caractérisée en ce que le groupement E² est le même ou est différent dans les motifs structuraux et représente le radical 1,4-phénylène ou le radical
    Figure imgb0028
     dans lequel R² représente un groupe alkyle ou alcoxy inférieur ayant chacun jusqu'à 4 atomes de carbone dans le fragment alkyle, ou F, Cl ou Br, ou le radical
    Figure imgb0029
     X' représentant le groupe -C(R¹)₂- dans lequel R¹ est un atome d'hydrogène ou un groupe alkyle en C₁-C₄, ou le groupement
    Figure imgb0030
  5. Membrane selon une ou plusieurs des revendications 1 à 4, contenant
    a) de la poly-N-vinylpyrrolidone et
    b) au moins un copolyaramide comportant au moins 3 motifs structuraux répétés de façon aléatoire, de formule (I), dans laquelle
    E¹   est un radical p-phénylène bivalent,
    E²,   dans les 3 motifs structuraux répétitifs, est, à chaque fois un radical p-phénylène bivalent, un radical de formule
    Figure imgb0031
     R² étant -CH₃, OCH₃, F, Cl ou Br, et un radical de formule
    Figure imgb0032
     dans lequel X' a la signification indiquée plus haut.
  6. Membrane selon la revendication 5, caractérisée en ce que le copolyaramide présente des motifs structuraux répétés
    Figure imgb0033
  7. Memorane selon une ou plusieurs des revendication 1 à 6, caractérisée en ce que le polyamide aromatique peut se trouver aussi bien sous forme de copolymère statistique que de copolymère séquencé ou greffé.
  8. Membrane selon une ou plusieurs des revendications 1 à 7, caractérisée en ce que l'alliage de polymères mélangés de façon homogène est préparé par polycondensation de diamines aromatiques et d'acides dicarboxyliques aromatiques ou de leurs dérivés aptes à la polycondensation, en présence de polyvinylpyrrolidone.
  9. Membrane selon une ou plusieurs des revendication 1 à 8, caractérisée en ce qu'elle contient de la polyvinylpyrrolidone ayant une masse moléculaire, indiquée en moyenne en poids, dans la plage allant de 1 000 à 3 000 000, de préférence de 40 000 à 200 000.
  10. Membrane selon une ou plusieurs des revendication 1 à 9, caractérisée en ce que la polyvinylpyrrolidone est contenue en proportions allant de 1 à 80 % en poids, de préférence de 5 à 60 % en poids, par rapport à la somme des composants.
  11. Membrane selon une ou plusieurs des revendication 1 à 10, caractérisée en ce qu'elle est asymétrique.
  12. Procédé pour la fabrication d'une membrane selon l'une des revendications 1 à 11, dans lequel on étale sous forme d'une couche liquide la solution de l'alliage de polymères, mélangés de façon homogène, sur un support plan, et on applique ensuite sur la couche liquide un liquide de précipitation qui est miscible au solvant de la solution, mais dans lequel l'alliage de polymères dissous, mélangés de façon homogène, est précipité sous forme d'une membrane, caractérisé en ce que, en tant que solvant pour l'alliage de polymères miscibles de façon homogène, on utilise des solvants aprotiques polaires du type amide, de préférence le N,N-diméthylacétamide ou en particulier la N-méthyl-2-pyrrolidone.
  13. Procédé selon la revendication 12, caractérisé en ce qu'une partie du solvant est évaporée avant la coagulation conduisant à la membrane.
  14. Procédé selon la revendication 12, caractérisé en ce que, en tant que liquide de précipitation, on utilise l'eau.
  15. Procédé selon l'une des revendications 12 à 14, caractérisé en ce que l'on fait agir le liquide de précipitation, sur la membrane précipitée par celui-ci, jusqu'à ce que pratiquement la totalité du solvant de celle-ci soit remplacée par du liquide de précipitation.
  16. Procédé selon l'une des revendications 12 à 15, caractérisé en ce que l'on élimine de la membrane le liquide de précipitation en la séchant dans un courant d'air.
  17. Procédé selon l'une des revendications 12 à 16, caractérisé en ce que la membrane est traitée avant le séchage par un plastifiant, de préférence le glycérol, et ensuite séchée.
  18. Procédé selon la revendication 16 ou 17, caractérisé en ce que la membrane est séchée à une température de 50°C.
  19. Procédé selon la revendication 15, caractérisé en ce que la membrane, dans laquelle pratiquement la totalité du solvant est remplacée par du liquide de précipitation, est soumise à un traitement thermique dans un liquide, pour la modification du pouvoir de rétention.
  20. Procédé selon la revendication 19, caractérisé en ce que le traitement thermique est effectué dans un liquide inerte.
  21. Procédé selon la revendication 15, caractérisé en ce que la membrane, dans laquelle pratiquement la totalité du solvant est remplacée par du liquide de précipitation, est soumise à un traitement thermique par de la vapeur d'eau, pour la modification du pouvoir de rétention.
  22. Procédé selon la revendication 17, caractérisé en ce que la membrane traitée par un plastifiant est soumise à un traitement thermique dans de l'air chaud ayant une humidité relative de l'air de 20 à 100 %, pour la modification du pouvoir de rétention.
  23. Procédé selon la revendication 19 ou 22, caractérisé en ce que le traitement thermique est effectué à une température dans la plage de 60 à 220°C, pendant une durée de 0,1 à 96 heures.
EP90101455A 1989-02-02 1990-01-25 Membrane semiperméable d'un alliage polymère mélangé demanière Expired - Lifetime EP0382009B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3903098 1989-02-02
DE3903098A DE3903098A1 (de) 1989-02-02 1989-02-02 Semipermeable membran aus einer homogen mischbaren polymerlegierung

Publications (2)

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EP0382009A1 EP0382009A1 (fr) 1990-08-16
EP0382009B1 true EP0382009B1 (fr) 1995-04-12

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US (1) US5152894A (fr)
EP (1) EP0382009B1 (fr)
JP (1) JPH03196822A (fr)
KR (1) KR0159772B1 (fr)
AT (1) ATE120982T1 (fr)
AU (1) AU630148B2 (fr)
CA (1) CA2008328C (fr)
DE (2) DE3903098A1 (fr)
DK (1) DK0382009T3 (fr)
ES (1) ES2071686T3 (fr)
FI (1) FI98497C (fr)
NO (1) NO174375C (fr)
NZ (1) NZ232314A (fr)

Families Citing this family (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW205513B (fr) * 1991-02-28 1993-05-11 Hoechst Ag
EP0543171B1 (fr) * 1991-10-26 1997-02-05 Hoechst Aktiengesellschaft Membranes en polyétheramide semi-perméables poreuses asymétriques
US5562826A (en) * 1991-10-26 1996-10-08 Hoechst Aktiengesellschaft Semipermeable, porous, asymmetric polyether amide membranes
DK0539870T3 (da) * 1991-10-26 1996-12-09 Hoechst Ag Hydrofile, asymmetriske, kemikaliebestandige polyaramidmembraner
EP0604882B1 (fr) * 1992-12-30 1998-08-26 Hoechst Aktiengesellschaft Membranes semi-perméables d'alliages polymères miscibles homogènes
DE4418843A1 (de) * 1994-05-30 1995-12-07 Hoechst Ag Poröse Membrane aus aromatischem Polyamid
DE4432859C2 (de) * 1994-09-15 1996-10-31 Seitz Filter Werke Symmetrische Mikrofiltrationsmembran aus aromatischem Polyamid und Verfahren zu ihrer Herstellung
DE19514540A1 (de) * 1995-04-20 1996-10-24 Gambro Dialysatoren Mit Hitze sterilisierbare Membran
DE19549001A1 (de) * 1995-12-28 1997-07-03 Hoechst Ag Verfahren zur Herstellung von Polyetheramidlösungen, unter Verwendung der Polyetheramidlösungen erhältliche dampfsterilisierbare Dialysemembranen sowie Verfahren zur Herstellung dieser Membranen
US6306301B1 (en) * 1996-10-31 2001-10-23 University Of Kentucky Research Foundation Silica-based membrane sorbent for heavy metal sequestration
US6139742A (en) * 1996-10-31 2000-10-31 University Of Kentucky Research Foundation Membrane-based sorbent for heavy metal sequestration
US6103121A (en) * 1996-10-31 2000-08-15 University Of Kentucky Research Foundation Membrane-based sorbent for heavy metal sequestration
DE19962319A1 (de) * 1999-12-23 2001-06-28 Clariant Gmbh Wasserverdünnbare Bindemittel und Beschichtungsmittel mit besonders schnell trocknenden Oberflächen, Verfahren zu deren Herstellung und deren Verwendung
TW504400B (en) * 2001-01-31 2002-10-01 Toshiba Corp Filtering apparatus, back wash method therefor, filtering device and power plant
JP2002306059A (ja) * 2001-04-17 2002-10-22 Gunze Kobunshi Corp 食品用ケーシングフイルム
NL1030288C2 (nl) * 2004-10-29 2006-10-09 Toray Industries Semipermeabel composietmembraan, productiewerkwijze daarvan, en element, fluïdumscheidingsinstallatie en werkwijze voor behandeling van water onder toepassing van hetzelfde.
WO2010065484A1 (fr) * 2008-12-04 2010-06-10 The University Of Akron Composition de polymère et membrane de dialyse formée à partir de la composition de polymère
US20120003361A1 (en) * 2009-03-17 2012-01-05 Ube Industries, Ltd. Polyamide resin composition, film comprising the same and polyamide-based laminate film
WO2011105278A1 (fr) * 2010-02-23 2011-09-01 東レ株式会社 Membrane semiperméable composite et son procédé de production
WO2011130206A1 (fr) * 2010-04-14 2011-10-20 The University Of Akron Composition de polymère comportant un agent phytochimique et membrane à dialyse formée à partir de la composition de polymère
CN104524995B (zh) * 2014-12-23 2017-01-04 大连理工大学 一种稳态结构分离膜及其制备方法
CN104801205B (zh) * 2015-04-20 2017-06-06 天津工业大学 一种同质增强型ppta中空纤维膜的制备方法
EP3095509A1 (fr) * 2015-05-18 2016-11-23 Defymed Membranes fonctionnalisées pour organes bioartificiels

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3526588A (en) * 1967-09-21 1970-09-01 Amicon Corp Macromolecular fractionation process
US3615024A (en) * 1968-08-26 1971-10-26 Amicon Corp High flow membrane
US4051300A (en) * 1973-09-03 1977-09-27 Gulf South Research Institute Hollow synthetic fibers
DE2751910B2 (de) * 1977-11-21 1979-09-20 Hoechst Ag, 6000 Frankfurt Permselektive, asymmetrische Hämofiltrationsmembran mit heteroporöser Struktur
US4900443A (en) * 1980-03-14 1990-02-13 Memtec North America Corporation Porous aramid membranes and emulsions useful for the casting thereof
JPS5858106A (ja) * 1981-09-30 1983-04-06 Kuraray Co Ltd 混合液の分離法
ES516206A0 (es) * 1981-10-21 1983-10-01 Du Pont "mejoras introducidas en un procedimiento para la preparacion de una membrana de osmosis inversa".
DE3149976A1 (de) * 1981-12-17 1983-06-30 Hoechst Ag, 6230 Frankfurt Makroporoese asymmetrische hydrophile membran aus synthetischem polymerisat
US4906375A (en) * 1984-07-14 1990-03-06 Fresenius, Ag Asymmetrical microporous hollow fiber for hemodialysis
DE3426331A1 (de) * 1984-07-17 1986-01-30 6380 Bad Homburg Fresenius AG Asymmetrische mikroporoese hohlfaser fuer die haemodialyse sowie verfahren zu ihrer herstellung
AU4787685A (en) * 1984-09-27 1986-04-10 E.I. Du Pont De Nemours And Company Aromatic polyamide membrane for reverse osmosis
JPS61271006A (ja) * 1985-05-28 1986-12-01 Nok Corp 限外口過膜
JPS6297624A (ja) * 1985-10-24 1987-05-07 イ−・アイ・デユポン・デ・ニモアス・アンド・カンパニ− ガス分離法及びその膜
ATE66633T1 (de) * 1985-12-23 1991-09-15 Gelman Sciences Inc Filtermembran und verfahren zu ihrer herstellung.
SE460521B (sv) * 1987-08-31 1989-10-23 Gambro Dialysatoren Permselektiv asymmetriskt membran samt foerfarande foer dess framstaellning
DE3802030A1 (de) * 1988-01-25 1989-07-27 Hoechst Ag Makroporoese, asymmetrische, hydrophile membran aus polyaramid

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FI98497C (fi) 1997-07-10
NO174375C (no) 1994-04-27
AU630148B2 (en) 1992-10-22
DE3903098A1 (de) 1990-08-16
ATE120982T1 (de) 1995-04-15
NZ232314A (en) 1992-06-25
NO174375B (no) 1994-01-17
ES2071686T3 (es) 1995-07-01
KR0159772B1 (ko) 1998-11-16
AU4900190A (en) 1990-08-09
CA2008328C (fr) 2001-04-10
KR900012982A (ko) 1990-09-03
DE59008872D1 (de) 1995-05-18
FI900483A0 (fi) 1990-01-31
NO900475D0 (no) 1990-02-01
DK0382009T3 (da) 1995-07-03
US5152894A (en) 1992-10-06
NO900475L (no) 1990-08-03
FI98497B (fi) 1997-03-27
JPH03196822A (ja) 1991-08-28
EP0382009A1 (fr) 1990-08-16
CA2008328A1 (fr) 1990-08-02

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